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US4870153A - Novel poly(aryl ether) polymers - Google Patents

Novel poly(aryl ether) polymers Download PDF

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US4870153A
US4870153A US07/111,344 US11134487A US4870153A US 4870153 A US4870153 A US 4870153A US 11134487 A US11134487 A US 11134487A US 4870153 A US4870153 A US 4870153A
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nickel
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Markus Matzner
George T. Kwiatkowski
Lloyd M. Robeson
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BP Corp North America Inc
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/38Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols
    • C08G65/40Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols from phenols (I) and other compounds (II), e.g. OH-Ar-OH + X-Ar-X, where X is halogen atom, i.e. leaving group
    • C08G65/4012Other compound (II) containing a ketone group, e.g. X-Ar-C(=O)-Ar-X for polyetherketones
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G61/00Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
    • C08G61/12Macromolecular compounds containing atoms other than carbon in the main chain of the macromolecule
    • C08G61/127Macromolecular compounds containing atoms other than carbon in the main chain of the macromolecule derived from carbon dioxide, carbonyl halide, carboxylic acids or their derivatives

Definitions

  • This invention is directed to novel poly(aryl ethers) that contain naphthalene, terephenylene and/or anthracenylene units within their chains.
  • Representative polymers are tough materials having excellent high temperature, oxidative and chemical resistance, and easy melt-fabricability.
  • Members of this class of resins are crystalline and display a high degree of order in the molten state or in solution.
  • Poly(aryl ethers) have been known for about two decades; they are tough linear polymers that possess a number of attractive features such as excellent high temperature resistance, good electrical properties, and very good hydrolytic stability.
  • Two poly(aryl ethers) are commercially available.
  • a poly(aryl ether sulfone) is available from Imperial Chemical Industries Limited. It has the formula (1) ##STR1## and is produced by polycondensation of 4,4'-dihydroxydiphenyl sulfone with 4,4'-dichlorodiphenyl sulfone as described in, for example, Canadian Pat. No. 847,963.
  • the polymer contains no aliphatic moieties and has a heat deflection temperature of approximately 210° C.
  • Another commercial poly(aryl ether) is available from Amoco Performance Products, Inc. under the trademark UDEL®. It corresponds to formula (2) and has a heat deflection temperature of about 180° C.
  • poly(aryl ether ketones) are engineering polymers that are highly crystalline [as opposed to the amorphous nature of (1) and (2)] with melting points above 300° C. Two of these crystalline poly(aryl ether ketones) are commercially available and are of the following structure: ##STR2##
  • PAE poly(aryl ethers)
  • PAEK is the acronym of poly(aryl ether ketone)
  • PEEK is the acronym of poly(ether ether ketone) in which the phenylene units in the structure are assumed.
  • both the poly(aryl ether sulfones) and the poly(aryl ether ketone) polymers are well known. They can be synthesized from a variety of starting materials; they show a wide range of glass transition (Tg) and melting (T m ) temperatures. They are tough materials and have a potential for a wide variety of uses; their favorable properties class them in the upper bracket of engineering polymers.
  • G is the desiduum of a dihydric phenol selected from the group consisting of ##STR5## wherein R represents a bond between aromatic carbon atoms, --O--, --S--, --S--S, or a divalent hydrocarbon radical having from 1 to 18 carbon atoms inclusive; and G' is the residuum of a dibromo or diiodobenzenoid compound selected from the group consisting of ##STR6## wherein R' represents a bond between aromatic carbon atoms, --O--, --S--, --S--S--, or a divalent hydrocarbon radical having from 1 to 18 carbon atoms inclusive; with the provisos that when R is --O--, R' is other than --O--; when G is (8), G' is (10); and when G' is (8), G is (9).
  • the polyarylene polyethers were claimed to possess excellent physical properties and thermal, oxidative, and chemical stability.
  • Poly(aryl ether) polymers were also prepared by the nickel catalyzed coupling of aryl polyhalides as described in U.S. Pat. No. 4,400,499.
  • the coupling reaction is performed in the presence of a reducing metal selected from the group consisting of zinc, magnesium and manganese or mixtures thereof, and in a liquid phase of an aprotic solvent under substantially anhydrous conditions.
  • the catalyst comprises a nickel compound and at least one ligand such as triarylphosphine; and an aromatic bidentate compound containing at least one ring nitrogen atom.
  • High molecular weight poly(aryl ethers) were obtained via this route.
  • the present invention is directed to novel poly(aryl ethers) containing naphthalene (11-13), terphenylene (14) and/or anthracenylene (15-18) units within their chains.
  • A is the group ##STR8## where the p's are integers and can be independently 1 or 2 and the m's are independently 0 or 1; T is as defined below.
  • the poly(aryl ethers) correspond to the general formula: ##STR9## wherein E is selected from the group of (11)-(18), and wherein E' is of the formulae ##STR10## E' may also be the same as E; T and T 1 can be the same or different and can be independently hydrogen, C 1 to C 4 alkyl; C 1 to C 4 alkoxy; phenyl, ⁇ -styryl and ⁇ -methylstyryl; or halogen.
  • Q represents a bond between aromatic carbon atoms, O, S, S--S, CH 2 or CO; with the proviso that when E is selected from the group of (11), (12) or (13) Q cannot be --CO-- when both m's are zero and n is one; n is an integer of 1 to 5; when n>1 the Q groups may be the same or different.
  • Naphthalene-base poly(aryl ethers) are also disclosed in Japanese Patent Applications Nos. 60/54,240, 60/116,475 and 62/39,632.
  • Representative poly(aryl ethers) of the present invention have excellent mechanical properties and very good thermal, oxidative and chemical resistance. Members of this class are highly crystalline; unexpectedly, many display a high degree of order in the molten state, or in solution, i.e., liquid crystalline (thermotropic) or lyotropic behavior.
  • the materials of the instant invention are preferably prepared via the Ullman route.
  • the reaction involves the cuprous catalyzed condensation of a diphenol dialkali metal salt with an aromatic dihalide, as illustrated in equation [II]: ##STR12##
  • the polyethers represented by formula (19) can, therefore, be prepared via the condensation of
  • thermoplastic polyarylene polyethers described herein can be prepared in a substantially equimolar reaction of a double alkali metal salt of the dihydric phenol with a diiodo- or a dibromobenzenoid compound in the presence of a cuprous salt or cuprous salt complex as a catalyst.
  • Any alkali metal salt of the dihydric phenol can be used as the one reactant.
  • the double alkali metal salt of the dihydric phenol should be dehydrated separately or in the reaction mass to insure anhydrous conditions.
  • the alkali metal salt can be prepared in situ in the inert diluent by reacting the dihydric phenol with an alkali metal, alkali metal hydroxide, alkali metal hydride, alkali metal carbonate or bicarbonate or alkali metal alkyl compound, and thereafter removing water, by distilling off a water-containing azeotrope from the reaction mass or by like techniques, to obtain anhydrous conditions.
  • Benzene, xylene, halogenated benzenes and other inert azeotrope forming organic liquids are suitable for this purpose.
  • the cuprous catalyst employed in the reaction can be a cuprous salt such as a cuprous halide, for example, cuprous chloride, cuprous bromide or cuprous iodide. Cuprous halides are preferred since they are highly effective but other cuprous salts can also be employed, for instance cuprous abietate (formed in situ by the reduction of cupric abietate), cuprous formate, cuprous acetate, and the like.
  • the cuprous catalyst can also be a complex of any of the foregoing cuprous salts obtained by combining the cuprous salt with a complexing agent such as pyridine, dimethyl acetamide, quinoline, dimethylformamide, N-methylpyrrolidone, and the like.
  • the quantity of the complexing agent can be varied widely but is usually in excess of the cuprous salt.
  • the amount of the cuprous catalyst employed is at least 0.01 mole percent based on the total monomers present.
  • Reaction temperatures above room temperature and generally above 100° C. are preferred. More preferred are temperatures between about 120° C. to about 360° C. Higher temperatures can, of course, be employed if desired, provided that care is taken to prevent degradation or decomposition of the reactants, the polymer and the solvents employed.
  • the polymer is recovered from the reaction mass in any convenient manner, such as by precipitation induced by cooling the reaction mass or by adding a nonsolvent for the polymer, or the solid polymer can be recovered by stripping off the solvent at reduced pressures and/or elevated temperatures.
  • the polymerization reaction results in the formation of the alkali metal bromide on each coupling reaction, it is preferred to either filter the salts from the polymer solution or to wash the polymer to substantially free it from these salts.
  • An alternative route to the poly(aryl ethers) of the present invention is the nickel coupling reaction of aromatic dihalides as described in U.S. Pat. No. 4,400,499 and in European Patent Application No. 25,460.
  • the method is useful for the preparation of polymers wherein at least one of the Q groups in formula (21) is a chemical bond; the method is particularly useful when at least one of the Q group is a chemical bond and n in formula (21) is 2 or 4. Examples are shown in equations [III] and [IV] where Q, T and T 1 are as previously defined. ##STR14##
  • Q' may be --O-- or --CO-- and may be the same or different; at least one Q' must be an oxygen bridge.
  • the polymerization reaction or coupling of the aryl dihalide, preferably dichloride, monomers proceeds by directly contacting the monomers with a catalyst mixture in the presence of a reducing metal selected from the group consisting of zinc, magnesium and manganese or mixtures thereof.
  • the polymerization reaction is conducted in the presence of a liquid phase of an aprotic solvent under substantially anhydrous conditions for a time and at a temperature sufficient to form the substantially linear high molecular weight thermoplastic polymers.
  • the catalyst mixture comprises an anhydrous nickel compound and at least one ligand selected from the group consisting of a triarylphosphine having from about 6 to about 14 carbon atoms in each aryl moiety and an aromatic bidentate compound containing at least one ring nitrogen atom and from about 5 to about 30 carbon atoms.
  • Suitable nickel compounds are nickel (O) complexes and those reducible by organometallic and metal reducing agents.
  • These compounds include nickel halides, that is, the chlorides, bromides and iodides, nickel sulfates, nickel phosphates, nickel carbonates, nickel salts or organic acids having 1 to 18 carbons, such as, nickel formate, nickel acetate, and nickel organic complexes such as nickel acetylacetonate, dichloro-bis(triphenylphosphine)nickel (II) and the like; and nickel (O) compounds such as bis(1,5-cyclooctadiene)nickel, tetrakis(triphenylphosphine)-nickel, and the like.
  • the anion of the nickel compounds is unimportant and merely serves to provide nickel ion to the catalyst mixture, but it must not interfere with the reaction of the nickel compound with the ligand.
  • the preferred anions are the halides.
  • Suitable triarylphosphines include triphenylphosphine, triphenylphosphines containing alkyl or alkoxy substituents having up to about 8 carbon atoms, and unsubstituted or alkyl- and alkoxy-substituted trinaphthyl phosphines.
  • Suitable bidentate compounds include 2,2'-bipyridine, 1,10-phenanthroline, 1,8-diazonaphthalene, 2-methylaminopyridine, and the like.
  • the preferred catalyst mixture comprises nickel chloride, triphenylphosphine and 2,2'-bipyridine.
  • the preferred ratio of gram atoms of nickel per mole of aryl polyhalide monomer is about 0.001 to about 0.1, with the most preferred range being 0.005 to 0.02.
  • the ratio of triarylphosphine to nickel can range from 0 to about 100, preferably from about 10 to about 50 moles per gram atom of nickel.
  • the ratio of bidentate ligand to nickel can range from 0 to about 5, preferably from about 0.2 to about 2, moles of bidentate ligand to gram atom of nickel.
  • triarylphosphine and aromatic bidentate ligand wherein the ratio of triarylphosphine to nickel varies from about 10 to about 50, and the ratio of bidentate ligand to nickel varies from about 0.5 to about 2 moles per gram atom of nickel.
  • the preferred reducing metal for use in the polymerization reaction of aryl polyhalide monomers is zinc metal although magnesium and manganese metals can also be used. It is preferred that the metal be in finely divided form with an average sieve size of 20 or finer when measured on the U.S. sieve scale. Although the stoichiometric amount of reducing metal required in this polymerization or coupling reaction is about 1 mole of reducing metal per mole of aryl polyhalide monomer i.e., dihalide, it is preferred to use a 50 percent excess or greater.
  • nickel (O) ligand complex believed to be the active catalyst can be formed in situ in the presence of an aryl polyhalide monomer solution, but the catalyst is preferably preformed in situ prior to the addition of the aryl polyhalide monomer solution.
  • a method for the determination of zero valent nickel is described by C. A. Tolman, J. Am. Chem. Soc. Volume 92, 2956 (1970). The presence of the active catalyst is indicated by the characteristic brown to red-brown color.
  • the polymerization or coupling reaction can take place at temperatures of from about 0° C. to about 250° C., preferably from about 25° C. to abut 120° C., and most preferably from about 40° C. to about 100° C. Pressure is not critical and so superatomspheric or subatmospheric pressures can be used as well as atmospheric pressure.
  • the reaction is preferably carried out in an inert atmosphere. Reaction times can vary from minutes to as long as several hours.
  • Inorganic salt promoters may be used with the triarylphosphines as ligands to reduce reaction times and/or temperatures.
  • Preferred inorganic salt promoters include alkali, alkaline earth, zinc, magnesium, manganese, and aluminum halides, or mixtures thereof. Iodides, chlorides and bromides are particularly preferred.
  • the amount of promoter when used can range from about 0.1 to about 1000 moles per gram atom of nickel with about 1 to about 100 moles of promoter being preferred. If desired, one can also employ alkali, alkaline earth, zinc, magnesium, manganese, and aluminum sulfates or phosphates or mixtures thereof as promoters.
  • the poly(aryl ethers) may be produced by the process described in, for example, U.S. Pat. No. 4,176,222. This process comprises heating in the temperature range of 100° to 400° C.,
  • the higher alkali metal carbonates or bicarbonates are thus selected from the group consisting of potassium, rubidium and cesium carbonates and bicarbonates. Preferred combinations are sodium carbonate or bicarbonate with potassium carbonate or cesium carbonate.
  • the alkali metal carbonates or bicarbonates should be anhydrous although, if hydrated salts are employed, where the polymerization temperature is relatively low, e.g., 100° to 250° C., the water should be removed, e.g., by heating under reduced pressure, prior to reaching the polymerization temperatures.
  • the total amount of alkali metal carbonate or bicarbonate employed should be such that there is at least 1 atom of alkali metal for each phenol group. Hence, there should be at least 1 mole of carbonate, or 2 moles of bicarbonate, per mole of aromatic diol.
  • An excess of carbonate or bicarbonate may be employed. Hence, there may be 1 to 1.2 atoms of alkali metal per phenol group. While the use of an excess of carbonate or bicarbonate may give rise to faster reactions, there is the attendant risk of cleavage of the resulting polymer, particularly when using high temperatures and/or the more active carbonates.
  • the amount of the second (higher) alkali metal carbonate or bicarbonate employed is such that there are 0.001 to about 0.2 gram atoms of the alkali metal of higher atomic number per gram atom of sodium.
  • a mixed carbonate for example sodium and potassium carbonate, may be employed as the second alkali metal carbonate.
  • one of the alkali metal atoms of the mixed carbonate is sodium
  • the amount of sodium in the mixed carbonate should be added to that in the sodium carbonate when determining the amount of the mixed carbonate to be employed.
  • the alkali metal of the second alkali metal carbonate or bicarbonate per gram atom of sodium is used.
  • the reaction can be carried out in the presence or absence of an inert solvent.
  • the solvent employed is an aliphatic or aromatic sulfoxide or sulfone of the formula
  • R 1 and R 2 are alkyl or aryl groups and may be the same or different.
  • R 1 and R 2 may together form a divalent radical.
  • Preferred solvents include dimethyl sulfoxide, dimethyl sulfone, sulfolane (1,1 dioxothiolan), or aromatic sulfones of the formula: ##STR17## where R' 2 is a direct link, an oxygen atom or two hydrogen atoms (one attached to each benzene ring) and R 3 and R' 3 , which may be the same or different, are hydrogen atoms and alkyl or phenyl groups.
  • aromatic sulfones examples include diphenylsulfone, dibenzothiophen dioxide, phenoxathiin dioxide and 4-phenylsulfonyl biphenyl.
  • Diphenylsulfone is the preferred solvent.
  • Ketone solvents such as benzophenone, are also useful.
  • the polymerization temperature is in the range of from about 100° C. to about 400° C. and will depend on the nature of the reactants and the solvent, if any, employed.
  • the preferred temperature is above 270° C.
  • the reactions are generally performed under atmospheric pressure. However, higher or lower pressures may be used.
  • the temperature may be desirable to commence polymerization at one temperature, e.g., between 200° C. and 250° C. and to increase the temperature as polymerization ensues. This is particularly necessary when making polymers having only a low solubility in the solvent. Thus, it is desirable to increase the temperature progressively to maintain the polymer in solution as its molecular weight increases.
  • the maximum polymerization temperature be below 350° C.
  • the nucleophilic polymerizations may also be performed in the presence of a base comprising sodium carbonate and/or bicarbonate and an alkali metal halide selected from potassium, rubidium or cesium fluoride or chloride, or combinations thereof, as described in U.S. Pat. No. 4,638,044.
  • a base comprising sodium carbonate and/or bicarbonate and an alkali metal halide selected from potassium, rubidium or cesium fluoride or chloride, or combinations thereof, as described in U.S. Pat. No. 4,638,044.
  • the poly(aryl ethers) of the instant invention can also be prepared via the known electrophilic processes. Examples are shown in equations (VII) and (VIII). ##STR18##
  • the poly(aryl ethers) may be produced by Friedel-Crafts reactions utilizing hydrogen fluoride-boron trifluoride catalysts as described, for example, in U.S. Pat. Nos. 3,953,400; 3,441,538; 3,442,857 and 3,516,966.
  • the poly(aryl ethers) may also be prepared according to the process as described in, for example, U.S. Defensive Publication No. T103,703 and U.S. Pat. No. 4,396,755. In such processes, reactants such as
  • the preparation may be conducted according to the process as described in U.S. Pat. No. 4,398,020. In such a process,
  • --Ar 1 -- is a divalent aromatic radical, such as naphthylene, terphenylene, anthracenylene, and the like;
  • Y is halogen, preferably chlorine; and
  • COY is an aromatically bound acyl halide group, which diacyl halide is polymerizable with at least one aromatic compound of (a) (ii), and
  • H--Ar'--H is an aromatic compound such as biphenyl, terphenyl, naphthalene, anthracene, or diphenyl ether, and H is an aromatically bound hydrogen atom, which compound is polymerizable with at least one diacyl halide of (a) (i), or
  • H--Ar"--H is an aromatic compound such as biphenyl, terphenyl, naphthalene, anthracene, diphenoxybiphenyl, diphenyl ether, diphenoxynaphthalene, diphenoxy-anthracene, and diphenoxybenzene, and H is an aromatically bound hydrogen atom
  • Y is halogen, preferably chlorine
  • COY is an aromatically bound acyl halide group, which monoacyl halide is self-polymerizable, or
  • the polymers may be prepared by Friedel-Crafts processes as described in, for example, U.S. Pat. Nos. 3,065,205; 3,419,462; 3,441,538; 3,442,857; 3,516,966 and 3,666,612.
  • a poly(aryl ether) is produced by Friedel-Crafts polymerization techniques using Friedel-Crafts catalysts such as aluminum trichloride, zinc chloride, ferric bromide, antimony pentachloride, titanium tetrachloride, etc. and a solvent.
  • the polymers may be prepared by reacting diphenyl ether, biphenyl, terphenyl, naphthalene, or anthracene, and, optionally, in addition to the above, any of the well-known aromatic co-reactants such as
  • acyldihalides include carbonyl chloride (phosgene), carbonyl bromide, carbonyl fluoride and oxaloyl chloride.
  • the preferred Friedel-Crafts catalysts are aluminum chloride, antimony pentachloride and ferric chloride.
  • Other Friedel-Crafts catalysts such as aluminum bromide, boron trifluoride, zinc chloride, antimony trichloride, ferric bromide, titanium tetrachloride, and stannic chloride, can also be used. In the preferred embodiment, excess of up to 100 mole percent of the acid catalyst is used.
  • the polymerization is generally carried out in the presence of a solvent.
  • the preferred organic solvent is 1,2-dichloroethane.
  • Other solvents such as symmetrical tetrachloroethane, o-dichlorobenzene, hydrogen fluoride, methylene chloride, trichloromethane, trichloroethylene, or carbon disulfide may be employed.
  • Co-solvents such as nitromethane, nitropropane, dimethyl formamide, sulfolane, etc. may be used. Concentrations as low as 3 to as high as 40 weight percent may be used.
  • the reactions may be carried out over a range of temperatures which are from about -40° C. to about 160° C. In general, it is preferred to carry out the reactions at a temperature in the range of -10° C. to about 30° C. In some cases it is advantageous to carry out the reactions at temperatures above 30° C. or below -10° C. Most preferably, the reactions are carried out at temperatures below about 0° C.
  • the reactions may be carried out at atmospheric pressure although higher or lower pressures may be used. Reaction times vary depending on the reactants, etc. Generally, reaction times of up to 6 hours and longer are preferred.
  • the poly(aryl ethers) of this invention exhibit reduced viscosities of from about 0.05 to about 5.0, and preferably, from about 0.1 to about 2.0 dl/g as measured in an appropriate solvent (1 g/100 ml) at 25° C.
  • the poly(aryl ethers) of this invention may include mineral fillers such as carbonates including chalk, calcite and dolomite; silicates including mica, talc, wollastonite, silicon dioxide; glass spheres, glass powders; aluminum, clay, quartz, and the like. Also, reinforcing fibers such as fiberglass, carbon fibers, and the like may be used.
  • the polymers may be blended with a variety of other polymers and may also include additives such as titanium dioxide, thermal stabilizers, ultraviolet light stabilizers, plasticizers, and the like.
  • the poly(aryl ethers) of this invention may be fabricated into any desired shape, i.e., moldings, coatings, films, or fibers.
  • reaction mass is diluted with 200 ml of toluene, and the polymer product is precipitated by adding ethanol containing about 5 volume percent of acetic acid.
  • the fluffy precipitate is washed with alcohol, hot water containing small amounts of acetic and hydrochloric acids, and again with hot alcohol-acetone.
  • the product is then dried at about 80° C., under vacuum, until constant weight. Material (44) is obtained in an almost quantitative yield.
  • This example illustrates the preparation of a poly(aryl ether) using the mucleophilic polycondensation method.
  • a mixture of 0.1 moles of the difluoride (45), 0.1 moles of phenylhydroquinone (46), 0.18 moles of sodium carbonate, 0.02 moles of potassium carbonate, 250 gms of diphenyl sulfone, and 100 ml of chlorobenzene is placed into a flask provided with a stirrer, thermometer, nitrogen inlet tube and a dean-stark trap, topped with a reflux condenser.
  • the mixture is heated with stirring under a dry nitrogen atmosphere to about 130°-140° C., at which point distillation of chlorobenzene/water begins.
  • the mixture is kept at about 150° C. for about one hour; during this time the chlorobenzene which has distilled out, is replaced by fresh chlorobenzene.
  • the temperature is then gradually increased without further addition of fresh chlorobenzene to about 280° C. (2 hours) and kept at 280° C. for 2.5 hours.
  • the reaction mixture is then heated to about 290° C. and kept at this temperature for 0.5 hours.
  • the contents of the flask are ground to a fine powder and extracted twice with acetone (each time: 1 liter of acetone, 1 hour of stirring), twice with 5 percent aqueous hydrochloric acid (700 ml of acid and 1 hour of stirring each time), followed by treatment with boiling water (1 liter of water, 1 hour of stirring) and then again with acetone (1 liter, 1 hour of stirring).
  • the polymer is then dried under vacuum at about 100° C. till constant weight. It is obtained in an essentially quantitative yield.
  • This example illustrates the preparation of a poly(aryl ether) using the electrophilic polycondensation method.
  • a three-liter glass lined reactor is charged with 0.50 moles of diphenyl ether (38), 0.50 moles of naphthalene-1,5-dicarbonyl chloride (37) and 1650 ml of 1,2-dichloroethane.
  • the mixture is cooled to 0.5° C. and 1.55 moles of aluminum chloride are slowly added while maintaining the temperature between 0°-5° C.
  • the resulting reaction mixture is held at 5°-10° C. for about 7 hours.
  • the ice bath is removed, and the reaction mixture is allowed to warm to ambient temperature (25° C.) where it is held for an additional 16 hours.
  • the reaction mixture is poured into 6 liters of ice water containing 200 ml of concentrated hydrochloric acid.
  • the resulting multiphase system is heated to about 85° C. to distill the 1,2-dichloroethane.
  • the polymer (39) is isolated by filtration, washed with water (2 ⁇ 1500 ml) and methanol (2 ⁇ 1500 ml), and dried in a vacuum oven at 100° C. It is obtained in an essentially quantitative yield.

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Abstract

Described herein are novel poly(aryl ether) polymers that contain naphthalene, terephenylene and/or anthracenylene units within their chains. Representative polymers are tough materials having excellent high temperature, oxidative and chemical resistance, and easy melt fabricability.

Description

FIELD OF THE INVENTION
This invention is directed to novel poly(aryl ethers) that contain naphthalene, terephenylene and/or anthracenylene units within their chains. Representative polymers are tough materials having excellent high temperature, oxidative and chemical resistance, and easy melt-fabricability. Members of this class of resins are crystalline and display a high degree of order in the molten state or in solution.
BACKGROUND OF THE INVENTION
Poly(aryl ethers) have been known for about two decades; they are tough linear polymers that possess a number of attractive features such as excellent high temperature resistance, good electrical properties, and very good hydrolytic stability. Two poly(aryl ethers) are commercially available. A poly(aryl ether sulfone) is available from Imperial Chemical Industries Limited. It has the formula (1) ##STR1## and is produced by polycondensation of 4,4'-dihydroxydiphenyl sulfone with 4,4'-dichlorodiphenyl sulfone as described in, for example, Canadian Pat. No. 847,963. The polymer contains no aliphatic moieties and has a heat deflection temperature of approximately 210° C. Another commercial poly(aryl ether) is available from Amoco Performance Products, Inc. under the trademark UDEL®. It corresponds to formula (2) and has a heat deflection temperature of about 180° C.
A closely related class of polymers, i.e., those wherein the sulfone group is partially or totally replaced by a keto group, is also known. The poly(aryl ether ketones) are engineering polymers that are highly crystalline [as opposed to the amorphous nature of (1) and (2)] with melting points above 300° C. Two of these crystalline poly(aryl ether ketones) are commercially available and are of the following structure: ##STR2##
Over the years, there has been developed a substantial body of patent and other literature directed to the formation and properties of poly(aryl ethers) (hereinafter called "PAE"). Some of the earliest work such as by Bonner, U.S. Pat. No. 3,065,205, involves the electrophillic aromatic substitution (viz. Friedel-Crafts catalyzed) reaction of aromatic diacylhalides with unsubstituted aromatic compounds such as diphenyl ether. The evolution of this class to a much broader range of PAEs was achieved by Johnson et al., Journal of Polymer Science, A-1, Vol. 5, 1967, pp. 2415-2427; Johnson et al., U.S. Pat. Nos. 4,108,837 and 4,175,175. Johnson et al. show that a very broad range of PAEs can be formed by the nucleophillic aroatic substitution (condensation) reaction of an activated aromatic dihalide and an aromatic diol. By this method, Johnson et al. created a host of new PAEs including a broad class of poly(aryl ether ketones) (hereinafter called PAEK's).
In recent years, there has developed a growing interest in PAEK's as evidenced by Dahl, U.S. Pat. Nos. 3,953,400; Dahl et al., 3,956,240; Dahl, 4,247,682; Rose et al., 4,320,224; Maresca, 4,339,568; Attwood et al., Polymer, 1981, Vol 22, August, pp. 1096-1103; Blundell et al., Polymer, 1983, Vol 24, Aug. pp. 953-958; AttWood et al., Polymer Preprints, 20, No. 1, April 1979, pp. 191-194; and Rueda et al., Polymer Communications, 1983, Vol 24, September, pp. 258-260. In early to mid-1970, Raychem Corp. commercially introduced a PAEK called STILAN, a polymer whose acronym is PEK, each ether and keto group being separated by 1,4-phenylene units. In 1978, Imperial Chemical Industries PLC (ICI) commerciallized a PAEK under the trademark Victrex PEEK. As PAEK is the acronym of poly(aryl ether ketone), PEEK is the acronym of poly(ether ether ketone) in which the phenylene units in the structure are assumed.
Thus, both the poly(aryl ether sulfones) and the poly(aryl ether ketone) polymers are well known. They can be synthesized from a variety of starting materials; they show a wide range of glass transition (Tg) and melting (Tm) temperatures. They are tough materials and have a potential for a wide variety of uses; their favorable properties class them in the upper bracket of engineering polymers.
As mentioned before, two of the most widely used preparative poly(aryl ether sulfone) and poly(aryl ether ketone) methods are the nucleophilic polycondensation, involving activated dihalobenzenoid compounds and bisphenoxides; and the electrophilic (Friedel-Crafts) route, such as the reaction of diacyl halides with aromatic reaction of diacyl halides with aromatic hydrocarbons, catalyzed by a Lewis acid. Two additional routes were described in the literature. The first of these is the Ullman polymerization; thus, the self-condensation of sodium p-bromophenoxide to poly(1,4-phenylene oxide) is claimed in U.S. Pat. No. 3,220,910; a cuprous chloride/pyridine complex was used as the catalyst: ##STR3##
The reaction of equation was also investigated by vanDort et al., European Polymer Journal, Vol. 4, pp. 275-287 (1968); and by Jurek and McGrath, Am. Chem. Soc., Div. Polymer Chemistry, Preprints, Vol. 28, No. 1, pp. 180-182 (1987). Linear polyarylene polyethers composed of recurring units having the formula ##STR4## and prepared via the Ullman route, are described in U.S. Pat. No. 3,332,909. In formula (7) G is the desiduum of a dihydric phenol selected from the group consisting of ##STR5## wherein R represents a bond between aromatic carbon atoms, --O--, --S--, --S--S, or a divalent hydrocarbon radical having from 1 to 18 carbon atoms inclusive; and G' is the residuum of a dibromo or diiodobenzenoid compound selected from the group consisting of ##STR6## wherein R' represents a bond between aromatic carbon atoms, --O--, --S--, --S--S--, or a divalent hydrocarbon radical having from 1 to 18 carbon atoms inclusive; with the provisos that when R is --O--, R' is other than --O--; when G is (8), G' is (10); and when G' is (8), G is (9). The polyarylene polyethers were claimed to possess excellent physical properties and thermal, oxidative, and chemical stability.
Poly(aryl ethers) of a somewhat similar structure, were disclosed in European Patent Application No. 222,536. These latter polymers were also prepared via the Ullman polycondensation.
Poly(aryl ether) polymers were also prepared by the nickel catalyzed coupling of aryl polyhalides as described in U.S. Pat. No. 4,400,499. The coupling reaction is performed in the presence of a reducing metal selected from the group consisting of zinc, magnesium and manganese or mixtures thereof, and in a liquid phase of an aprotic solvent under substantially anhydrous conditions. The catalyst comprises a nickel compound and at least one ligand such as triarylphosphine; and an aromatic bidentate compound containing at least one ring nitrogen atom. High molecular weight poly(aryl ethers) were obtained via this route.
The Invention
The present invention is directed to novel poly(aryl ethers) containing naphthalene (11-13), terphenylene (14) and/or anthracenylene (15-18) units within their chains. ##STR7## In the structures (11)-(18) A is the group ##STR8## where the p's are integers and can be independently 1 or 2 and the m's are independently 0 or 1; T is as defined below.
The poly(aryl ethers) correspond to the general formula: ##STR9## wherein E is selected from the group of (11)-(18), and wherein E' is of the formulae ##STR10## E' may also be the same as E; T and T1 can be the same or different and can be independently hydrogen, C1 to C4 alkyl; C1 to C4 alkoxy; phenyl, α-styryl and α-methylstyryl; or halogen. Q represents a bond between aromatic carbon atoms, O, S, S--S, CH2 or CO; with the proviso that when E is selected from the group of (11), (12) or (13) Q cannot be --CO-- when both m's are zero and n is one; n is an integer of 1 to 5; when n>1 the Q groups may be the same or different.
It should be noted that the poly(aryl ether ketones) obtained from the difluorobenzoyl derivative (22) and the diphenol (23) were described recently ##STR11## see B. J. Jensen, P. M. Hergenrother and S. J. Havens, talk presented at the "Symposium of Recent advances in Polyimides and Other High Performance Polymers", Reno, Nevada, July 13-16, 1987.
Naphthalene-base poly(aryl ethers) are also disclosed in Japanese Patent Applications Nos. 60/54,240, 60/116,475 and 62/39,632.
Representative poly(aryl ethers) of the present invention have excellent mechanical properties and very good thermal, oxidative and chemical resistance. Members of this class are highly crystalline; unexpectedly, many display a high degree of order in the molten state, or in solution, i.e., liquid crystalline (thermotropic) or lyotropic behavior.
The materials of the instant invention are preferably prepared via the Ullman route. The reaction involves the cuprous catalyzed condensation of a diphenol dialkali metal salt with an aromatic dihalide, as illustrated in equation [II]: ##STR12##
The polyethers represented by formula (19) can, therefore, be prepared via the condensation of
(a) the dihalide X--E--X, wherein X is halogen, with the dialkali metal salt of the diol HO--E'--OH; or via the condensation of
(b) the dihalide X--E'--X with the dialkali metal salt of the diol HO--E--OH.
Obviously, a variety of other combinations of reactants, obvious to those skilled in the art, are possible. Thus, one may use the halophenols (25) which will lead to poly(aryl ethers) ##STR13## wherein E and E' are the same. It is also contemplated in this invention to use a mixture of two or more different dihydric phenols and/or two or more different aromatic dihalides to accomplish the same ends as above. Thus, when referred to above, the E (and E') residuum in the polymer structure can actually be the same or different aromatic residua.
While not wishing to be bound by any scientific theory or explanation of the polymerization, it is believed, as indicated in a study (H. Weingarten, J. Org. Chem., Vol. 29, p. 977 (1964); ibid., Vol. 29, p. 3624 (1964)) on the mechanism of the Ullman reaction, that Cu+ is the active catalytic species; it is assumed that it coordinates with the π system of the aromatic halide, thus facilitating carbonhalogen cleavage. With the Ullman reaction, the order of ease of halide replacement is I>Br>Cl>>F. This is actually the reverse of the order observed for polyether formation in typical nucleophilic polymerizations. Hence, the diiodoand the dibromo-monomers are the preferred dihaloaromatic materials.
The thermoplastic polyarylene polyethers described herein can be prepared in a substantially equimolar reaction of a double alkali metal salt of the dihydric phenol with a diiodo- or a dibromobenzenoid compound in the presence of a cuprous salt or cuprous salt complex as a catalyst. Any alkali metal salt of the dihydric phenol can be used as the one reactant. For purposes of this invention, to obtain high molecular weight polymers, it is preferred to conduct the reaction under substantially anhydrous conditions and in an oxygen free atmosphere.
Generally the reaction is carried out in an inert diluent in which the alkali metal salt of the dihydric phenol and/or the dibromo or diodobeneenoid compound is partly soluble. Suitable solvents include benzophenone, diphenyl ether, benzonitrile, dialkoxy benzenes in which each alkoxy group contains from 1 to 4 carbon atoms, trialkoxy benzenes in which each alkoxy group contains 1 to 4 carbon atoms, and the typical aprotic solvents such as diphenyl sulfone, dimethylsulfoxide, dimethylsulfone, diethylsulfoxide, diethylsulfone, diisopropylsulfone, tetrahydrothiophene-1,1-dioxide (commonly called tetramethylene sulfone or sulfolane), tetrahydrothiophene-1 monoxide, N,N-dimethylacetamide, N-methylpyrrolidone, N-cyclohexylpyrrolidone, and the like.
The double alkali metal salt of the dihydric phenol, if it is present as the hydrate, should be dehydrated separately or in the reaction mass to insure anhydrous conditions. Similarly, the alkali metal salt can be prepared in situ in the inert diluent by reacting the dihydric phenol with an alkali metal, alkali metal hydroxide, alkali metal hydride, alkali metal carbonate or bicarbonate or alkali metal alkyl compound, and thereafter removing water, by distilling off a water-containing azeotrope from the reaction mass or by like techniques, to obtain anhydrous conditions. Benzene, xylene, halogenated benzenes and other inert azeotrope forming organic liquids are suitable for this purpose.
The cuprous catalyst employed in the reaction can be a cuprous salt such as a cuprous halide, for example, cuprous chloride, cuprous bromide or cuprous iodide. Cuprous halides are preferred since they are highly effective but other cuprous salts can also be employed, for instance cuprous abietate (formed in situ by the reduction of cupric abietate), cuprous formate, cuprous acetate, and the like. The cuprous catalyst can also be a complex of any of the foregoing cuprous salts obtained by combining the cuprous salt with a complexing agent such as pyridine, dimethyl acetamide, quinoline, dimethylformamide, N-methylpyrrolidone, and the like. The quantity of the complexing agent can be varied widely but is usually in excess of the cuprous salt. The amount of the cuprous catalyst employed is at least 0.01 mole percent based on the total monomers present.
The reaction between the diiodo- or the dibromobenzenoid compound and the alkali metal salt of the dihydric phenol proceeds on an equimolar basis. This can be slightly varied, but as little a variation as 5 percent away from equal molar amounts, seriously reduces the molecular weight of the polymers.
Reaction temperatures above room temperature and generally above 100° C. are preferred. More preferred are temperatures between about 120° C. to about 360° C. Higher temperatures can, of course, be employed if desired, provided that care is taken to prevent degradation or decomposition of the reactants, the polymer and the solvents employed.
The polymer is recovered from the reaction mass in any convenient manner, such as by precipitation induced by cooling the reaction mass or by adding a nonsolvent for the polymer, or the solid polymer can be recovered by stripping off the solvent at reduced pressures and/or elevated temperatures.
Since the polymerization reaction results in the formation of the alkali metal bromide on each coupling reaction, it is preferred to either filter the salts from the polymer solution or to wash the polymer to substantially free it from these salts.
An alternative route to the poly(aryl ethers) of the present invention is the nickel coupling reaction of aromatic dihalides as described in U.S. Pat. No. 4,400,499 and in European Patent Application No. 25,460. The method is useful for the preparation of polymers wherein at least one of the Q groups in formula (21) is a chemical bond; the method is particularly useful when at least one of the Q group is a chemical bond and n in formula (21) is 2 or 4. Examples are shown in equations [III] and [IV] where Q, T and T1 are as previously defined. ##STR14## In the formulae above Q' may be --O-- or --CO-- and may be the same or different; at least one Q' must be an oxygen bridge.
A variety of para-haloghenoxy and/or para-halophenyl carbonyl derivatives of compounds (11)-(18) can be used in a similar fashion. ##STR15##
Derivatives similar to (30) and based on the compounds (11-18) can be used in an analogous manner. In formulae (30) and (31), Q and Q' are as defined above and may be the same or different; at least one Q or Q' group must be an oxygen bridge.
The polymerization reaction or coupling of the aryl dihalide, preferably dichloride, monomers proceeds by directly contacting the monomers with a catalyst mixture in the presence of a reducing metal selected from the group consisting of zinc, magnesium and manganese or mixtures thereof. The polymerization reaction is conducted in the presence of a liquid phase of an aprotic solvent under substantially anhydrous conditions for a time and at a temperature sufficient to form the substantially linear high molecular weight thermoplastic polymers.
The catalyst mixture comprises an anhydrous nickel compound and at least one ligand selected from the group consisting of a triarylphosphine having from about 6 to about 14 carbon atoms in each aryl moiety and an aromatic bidentate compound containing at least one ring nitrogen atom and from about 5 to about 30 carbon atoms. Suitable nickel compounds are nickel (O) complexes and those reducible by organometallic and metal reducing agents. These compounds include nickel halides, that is, the chlorides, bromides and iodides, nickel sulfates, nickel phosphates, nickel carbonates, nickel salts or organic acids having 1 to 18 carbons, such as, nickel formate, nickel acetate, and nickel organic complexes such as nickel acetylacetonate, dichloro-bis(triphenylphosphine)nickel (II) and the like; and nickel (O) compounds such as bis(1,5-cyclooctadiene)nickel, tetrakis(triphenylphosphine)-nickel, and the like. The anion of the nickel compounds is unimportant and merely serves to provide nickel ion to the catalyst mixture, but it must not interfere with the reaction of the nickel compound with the ligand. The preferred anions are the halides. Suitable triarylphosphines include triphenylphosphine, triphenylphosphines containing alkyl or alkoxy substituents having up to about 8 carbon atoms, and unsubstituted or alkyl- and alkoxy-substituted trinaphthyl phosphines. Suitable bidentate compounds include 2,2'-bipyridine, 1,10-phenanthroline, 1,8-diazonaphthalene, 2-methylaminopyridine, and the like. The preferred catalyst mixture comprises nickel chloride, triphenylphosphine and 2,2'-bipyridine.
The preferred ratio of gram atoms of nickel per mole of aryl polyhalide monomer is about 0.001 to about 0.1, with the most preferred range being 0.005 to 0.02. The ratio of triarylphosphine to nickel can range from 0 to about 100, preferably from about 10 to about 50 moles per gram atom of nickel. The ratio of bidentate ligand to nickel can range from 0 to about 5, preferably from about 0.2 to about 2, moles of bidentate ligand to gram atom of nickel. It is preferred to use a combination of triarylphosphine and aromatic bidentate ligand, wherein the ratio of triarylphosphine to nickel varies from about 10 to about 50, and the ratio of bidentate ligand to nickel varies from about 0.5 to about 2 moles per gram atom of nickel.
The preferred reducing metal for use in the polymerization reaction of aryl polyhalide monomers is zinc metal although magnesium and manganese metals can also be used. It is preferred that the metal be in finely divided form with an average sieve size of 20 or finer when measured on the U.S. sieve scale. Although the stoichiometric amount of reducing metal required in this polymerization or coupling reaction is about 1 mole of reducing metal per mole of aryl polyhalide monomer i.e., dihalide, it is preferred to use a 50 percent excess or greater.
While not wishing to be bound by any scientific theory or explanation of the mechanism of the polymerization or coupling reaction of this invention, it is believed that the combination of nickel compound, ligand and reducing metal provides nickel in a zero valent state, a form which in an anhydrous aprotic medium enables the coupling of aryl polyhalide monomers to take place in excellent yields. The nickel (O) ligand complex believed to be the active catalyst can be formed in situ in the presence of an aryl polyhalide monomer solution, but the catalyst is preferably preformed in situ prior to the addition of the aryl polyhalide monomer solution. A method for the determination of zero valent nickel is described by C. A. Tolman, J. Am. Chem. Soc. Volume 92, 2956 (1970). The presence of the active catalyst is indicated by the characteristic brown to red-brown color.
The polymerization or coupling reaction can take place at temperatures of from about 0° C. to about 250° C., preferably from about 25° C. to abut 120° C., and most preferably from about 40° C. to about 100° C. Pressure is not critical and so superatomspheric or subatmospheric pressures can be used as well as atmospheric pressure. The reaction is preferably carried out in an inert atmosphere. Reaction times can vary from minutes to as long as several hours. Inorganic salt promoters may be used with the triarylphosphines as ligands to reduce reaction times and/or temperatures.
Preferred inorganic salt promoters include alkali, alkaline earth, zinc, magnesium, manganese, and aluminum halides, or mixtures thereof. Iodides, chlorides and bromides are particularly preferred. The amount of promoter when used can range from about 0.1 to about 1000 moles per gram atom of nickel with about 1 to about 100 moles of promoter being preferred. If desired, one can also employ alkali, alkaline earth, zinc, magnesium, manganese, and aluminum sulfates or phosphates or mixtures thereof as promoters.
The classical nucleophilic polycondensation reaction of activated dihalobenzenoid compounds with diphenoxides in an additional route whereby certain of the novel poly(aryl ethers) can be prepared. The method is applicable to keto-containing polymers, where one of the starting materials is either an activated dihalobenzenoid monomer, or a halophenol whose halogen atom is in position ortho- or para to the carbonyl function. Examples are shown in equations [V] and [VI]. ##STR16##
Thus, the poly(aryl ethers) may be produced by the process described in, for example, U.S. Pat. No. 4,176,222. This process comprises heating in the temperature range of 100° to 400° C.,
(i) at least one bisphenol and at least one dihalobenzenoid compound, and/or
(ii) at least one halophenol in which in the dihalobenzenoid compound or halophenol, the halogen atoms are activated by --CO-- groups ortho or para thereto, with a mixture of sodium carbonate or bicarbonate and a second alkali metal carbonate or bicarbonate, the alkali metal of said second alkali metal carbonate or bicarbonate having a higher atomic number than that of sodium, the amount of said second alkali metal carbonate or bicarbonate being such that there are 0.001 to 0.2 gram atoms of said alkali metal of higher atomic number per gram atom of sodium, the total amount of alkali metal carbonate or bicarbonate being such that there is at least one alkali metal atom for each phenol group present, and thereafter separating the polymer from the alkali metal halide.
The higher alkali metal carbonates or bicarbonates are thus selected from the group consisting of potassium, rubidium and cesium carbonates and bicarbonates. Preferred combinations are sodium carbonate or bicarbonate with potassium carbonate or cesium carbonate.
The alkali metal carbonates or bicarbonates should be anhydrous although, if hydrated salts are employed, where the polymerization temperature is relatively low, e.g., 100° to 250° C., the water should be removed, e.g., by heating under reduced pressure, prior to reaching the polymerization temperatures.
Where high polymerization temperatures (>250° C.) are used, it is not necessary to dehydrate the carbonate or bicarbonate first as any water is driven off rapidly before it can adversely affect the course of the polymerization reaction.
The total amount of alkali metal carbonate or bicarbonate employed should be such that there is at least 1 atom of alkali metal for each phenol group. Hence, there should be at least 1 mole of carbonate, or 2 moles of bicarbonate, per mole of aromatic diol.
An excess of carbonate or bicarbonate may be employed. Hence, there may be 1 to 1.2 atoms of alkali metal per phenol group. While the use of an excess of carbonate or bicarbonate may give rise to faster reactions, there is the attendant risk of cleavage of the resulting polymer, particularly when using high temperatures and/or the more active carbonates.
As stated above, the amount of the second (higher) alkali metal carbonate or bicarbonate employed is such that there are 0.001 to about 0.2 gram atoms of the alkali metal of higher atomic number per gram atom of sodium.
Thus, when using a mixture of carbonates, e.g., sodium carbonate and cesium carbonate, there should be 0.1 to about 20 moles of cesium carbonate per 100 moles of sodium carbonate. Likewise, when using a mixture of a bicarbonate and a carbonate, e.g., sodium bicarbonate and potassium carbonate, there should be 0.05 to 10 moles of potassium carbonate per 100 moles of sodium bicarbonate.
A mixed carbonate, for example sodium and potassium carbonate, may be employed as the second alkali metal carbonate. In this case, where one of the alkali metal atoms of the mixed carbonate is sodium, the amount of sodium in the mixed carbonate should be added to that in the sodium carbonate when determining the amount of the mixed carbonate to be employed.
Preferably, from 0.005 to 0.1 gram atoms of the alkali metal of the second alkali metal carbonate or bicarbonate per gram atom of sodium is used.
The reaction can be carried out in the presence or absence of an inert solvent.
Preferably, the solvent employed is an aliphatic or aromatic sulfoxide or sulfone of the formula
R.sub.1 --S(O).sub.x --R.sub.2
where x is 1 or 2 and R1 and R2 are alkyl or aryl groups and may be the same or different. R1 and R2 may together form a divalent radical. Preferred solvents include dimethyl sulfoxide, dimethyl sulfone, sulfolane (1,1 dioxothiolan), or aromatic sulfones of the formula: ##STR17## where R'2 is a direct link, an oxygen atom or two hydrogen atoms (one attached to each benzene ring) and R3 and R'3, which may be the same or different, are hydrogen atoms and alkyl or phenyl groups. Examples of such aromatic sulfones include diphenylsulfone, dibenzothiophen dioxide, phenoxathiin dioxide and 4-phenylsulfonyl biphenyl. Diphenylsulfone is the preferred solvent. Ketone solvents such as benzophenone, are also useful.
The polymerization temperature is in the range of from about 100° C. to about 400° C. and will depend on the nature of the reactants and the solvent, if any, employed. The preferred temperature is above 270° C. The reactions are generally performed under atmospheric pressure. However, higher or lower pressures may be used.
For the production of some polymers, it may be desirable to commence polymerization at one temperature, e.g., between 200° C. and 250° C. and to increase the temperature as polymerization ensues. This is particularly necessary when making polymers having only a low solubility in the solvent. Thus, it is desirable to increase the temperature progressively to maintain the polymer in solution as its molecular weight increases.
To minimize cleavage reactions it is preferred that the maximum polymerization temperature be below 350° C.
The nucleophilic polymerizations may also be performed in the presence of a base comprising sodium carbonate and/or bicarbonate and an alkali metal halide selected from potassium, rubidium or cesium fluoride or chloride, or combinations thereof, as described in U.S. Pat. No. 4,638,044.
Other base systems, useful in the nucleophilic polycondensation reactions, are
(1) a mixture of
(a) a lithium and/or an alkaline earth metal carbonate or bicarbonate, and
(b) a sodium, potassium, rubidium, and/or a cesium carbonate or bicarbonate, as described in German Patent Application No. 3,342,433;
(2) a mixture of sodium or an alkaline earth metal carbonate or bicarbonate and a potassium, rubidium or cesium salt of an organic acid, as described in U.S. patent application, Ser. No. 037,839, filed Apr. 13, 1987 in the names of Paul A. Winslow, Donald R. Kelsey and Markus Matzner, titled "Improved Process for Preparing Poly(aryl ethers) and Poly(aryl ether ketones)", commonly assigned; and
(3) a mixture of sodium or an alkaline earth metal carbonate or bicarbonate and a lithium, sodium or alkaline earth metal salt of an organic acid, optionally in combination with a catalytic amount of a potassium, cesium or rubidium salt catalyst, as described in the aforementioned U.S. patent application, Ser. No. 037,839.
All of the above reactions may be advantageously performed in the presence of small amounts of cupric or cuprous ions.
The poly(aryl ethers) of the instant invention can also be prepared via the known electrophilic processes. Examples are shown in equations (VII) and (VIII). ##STR18## The poly(aryl ethers) may be produced by Friedel-Crafts reactions utilizing hydrogen fluoride-boron trifluoride catalysts as described, for example, in U.S. Pat. Nos. 3,953,400; 3,441,538; 3,442,857 and 3,516,966.
The poly(aryl ethers) may also be prepared according to the process as described in, for example, U.S. Defensive Publication No. T103,703 and U.S. Pat. No. 4,396,755. In such processes, reactants such as
(a) an aromatic monocarboxylic acid;
(b) a mixture of at least one aromatic dicarboxylic acid and an aromatic hydrocarbon; and
(c) combinations of (a) and (b) are reacted in the presence of a fluoroalkane sulphonic acid, particularly trifluoromethane sulphonic acid.
In another embodiment, the preparation may be conducted according to the process as described in U.S. Pat. No. 4,398,020. In such a process,
(a) a mixture of substantially equimolar amounts of
(i) at least one aromatic diacyl halide of formula
YOC--Ar.sub.1 --COY
where --Ar1 -- is a divalent aromatic radical, such as naphthylene, terphenylene, anthracenylene, and the like; Y is halogen, preferably chlorine; and COY is an aromatically bound acyl halide group, which diacyl halide is polymerizable with at least one aromatic compound of (a) (ii), and
(ii) at least one aromatic compound of the formula
H--Ar'--H
wherein H--Ar'--H is an aromatic compound such as biphenyl, terphenyl, naphthalene, anthracene, or diphenyl ether, and H is an aromatically bound hydrogen atom, which compound is polymerizable with at least one diacyl halide of (a) (i), or
(b) at least one aromatic monoacyl halide of the formula
H--Ar"--COY
where H--Ar"--H is an aromatic compound such as biphenyl, terphenyl, naphthalene, anthracene, diphenoxybiphenyl, diphenyl ether, diphenoxynaphthalene, diphenoxy-anthracene, and diphenoxybenzene, and H is an aromatically bound hydrogen atom, Y is halogen, preferably chlorine, and COY is an aromatically bound acyl halide group, which monoacyl halide is self-polymerizable, or
(c) a combination of (a) and (b) is reacted in the presence of a fluoroalkane sulphonic acid.
Additionally, the polymers may be prepared by Friedel-Crafts processes as described in, for example, U.S. Pat. Nos. 3,065,205; 3,419,462; 3,441,538; 3,442,857; 3,516,966 and 3,666,612. In these patents, a poly(aryl ether) is produced by Friedel-Crafts polymerization techniques using Friedel-Crafts catalysts such as aluminum trichloride, zinc chloride, ferric bromide, antimony pentachloride, titanium tetrachloride, etc. and a solvent.
The polymers may be prepared by reacting diphenyl ether, biphenyl, terphenyl, naphthalene, or anthracene, and, optionally, in addition to the above, any of the well-known aromatic co-reactants such as
diphenyl sulfide, 4,4'-diphenoxybiphenyl,
diphenyl methane, 1,4-diphenoxybenzene,
1,3-diphenoxybenzene, 1-phenoxynaphthalene,
4,4'-diphenoxybenzophenone,
4,4'-diphenoxy dibenzoyl benzene,
1,5-diphenoxynaphthalene,
1-phenoxyanthracene, 1,5-diphenoxyanthracene,
1,6-diphenoxyanthracene, and the like.
Similarly, the following compounds are diacyl halides which may be used as reactants:
terephthaloyl chloride, isophthaloyl chloride,
thio-bis(4,4'-benzoyl chloride),
benzophenone-4,4'-di(carbonyl chloride),
oxy-bis(3,3'-benzoyl chloride),
diphenyl-3,3'-di(carbonyl chloride),
benzophenone-3,3'-di(carbonyl chloride),
thio-bis(3,4'-benzoyl chloride),
diphenyl-3,4'-di(carbonyl chloride),
naphthalene-1,6-di(carbonyl chloride),
naphthalene-1,5-di(carbonyl chloride),
naphthalene-2,6-di(carbonyl chloride),
naphthalene-2,7-di(carbonyl chloride),
oxy-bis[7,7'-naphthalene-2,2'-di(carbonyl chloride)],
thio-bis[5,5'-naphthalene-1,1'-di(carbonyl chloride)],
7,7'-binaphthyl-2,2'-di(carbonyl chloride),
diphenyl-4,4'-di(carbonyl chloride),
carbonyl-bis[7,7'-naphthalene-2,2'-di(carbonyl chloride)],
sulfonyl-bis[6,6'-naphthalene-2,2'-di(carbonyl chloride)],
anthracene-1,5-di(carbonyl chloride) and the like.
Illustrative of suitable acyldihalides include carbonyl chloride (phosgene), carbonyl bromide, carbonyl fluoride and oxaloyl chloride.
The preferred Friedel-Crafts catalysts are aluminum chloride, antimony pentachloride and ferric chloride. Other Friedel-Crafts catalysts, such as aluminum bromide, boron trifluoride, zinc chloride, antimony trichloride, ferric bromide, titanium tetrachloride, and stannic chloride, can also be used. In the preferred embodiment, excess of up to 100 mole percent of the acid catalyst is used.
The polymerization is generally carried out in the presence of a solvent. The preferred organic solvent is 1,2-dichloroethane. Other solvents such as symmetrical tetrachloroethane, o-dichlorobenzene, hydrogen fluoride, methylene chloride, trichloromethane, trichloroethylene, or carbon disulfide may be employed. Co-solvents such as nitromethane, nitropropane, dimethyl formamide, sulfolane, etc. may be used. Concentrations as low as 3 to as high as 40 weight percent may be used.
The reactions may be carried out over a range of temperatures which are from about -40° C. to about 160° C. In general, it is preferred to carry out the reactions at a temperature in the range of -10° C. to about 30° C. In some cases it is advantageous to carry out the reactions at temperatures above 30° C. or below -10° C. Most preferably, the reactions are carried out at temperatures below about 0° C. The reactions may be carried out at atmospheric pressure although higher or lower pressures may be used. Reaction times vary depending on the reactants, etc. Generally, reaction times of up to 6 hours and longer are preferred.
The poly(aryl ethers) of this invention exhibit reduced viscosities of from about 0.05 to about 5.0, and preferably, from about 0.1 to about 2.0 dl/g as measured in an appropriate solvent (1 g/100 ml) at 25° C.
The poly(aryl ethers) of this invention may include mineral fillers such as carbonates including chalk, calcite and dolomite; silicates including mica, talc, wollastonite, silicon dioxide; glass spheres, glass powders; aluminum, clay, quartz, and the like. Also, reinforcing fibers such as fiberglass, carbon fibers, and the like may be used. The polymers may be blended with a variety of other polymers and may also include additives such as titanium dioxide, thermal stabilizers, ultraviolet light stabilizers, plasticizers, and the like.
The poly(aryl ethers) of this invention may be fabricated into any desired shape, i.e., moldings, coatings, films, or fibers.
EXAMPLES
The following examples serve to give specific illustrations of the practice of this invention but they are not intended in any way to limit the scope of this invention.
Example 1
This example illustrates the preparation of a poly(aryl ether) using the Ullman reaction. ##STR19##
Into a flask are placed 0.1 moles of the anhydrous disodium salt of (42), 150 gms of benzophenone, and 0.1 moles of p-dibromobenzene (43). The flask is sparged with nitrogen, and 10 ml of a pyridine solution of cuprous chloride (about 1 mmole) are added. The reaction mass is heated for about 6 hours at 185°-215° C. after which 5 mole percent of bromobenzene (i.e., 0.005 moles) are added; heating is continued for an additional hour. The obtained polymer is thus essentially devoid of any undesirable phenoxide end-groups. The reaction mass is diluted with 200 ml of toluene, and the polymer product is precipitated by adding ethanol containing about 5 volume percent of acetic acid. The fluffy precipitate is washed with alcohol, hot water containing small amounts of acetic and hydrochloric acids, and again with hot alcohol-acetone. The product is then dried at about 80° C., under vacuum, until constant weight. Material (44) is obtained in an almost quantitative yield.
Example 2
This example illustrates the preparation of a poly(aryl ether) using the mucleophilic polycondensation method. ##STR20## A mixture of 0.1 moles of the difluoride (45), 0.1 moles of phenylhydroquinone (46), 0.18 moles of sodium carbonate, 0.02 moles of potassium carbonate, 250 gms of diphenyl sulfone, and 100 ml of chlorobenzene is placed into a flask provided with a stirrer, thermometer, nitrogen inlet tube and a dean-stark trap, topped with a reflux condenser. The mixture is heated with stirring under a dry nitrogen atmosphere to about 130°-140° C., at which point distillation of chlorobenzene/water begins. The mixture is kept at about 150° C. for about one hour; during this time the chlorobenzene which has distilled out, is replaced by fresh chlorobenzene. The temperature is then gradually increased without further addition of fresh chlorobenzene to about 280° C. (2 hours) and kept at 280° C. for 2.5 hours. The reaction mixture is then heated to about 290° C. and kept at this temperature for 0.5 hours. After cooling, the contents of the flask are ground to a fine powder and extracted twice with acetone (each time: 1 liter of acetone, 1 hour of stirring), twice with 5 percent aqueous hydrochloric acid (700 ml of acid and 1 hour of stirring each time), followed by treatment with boiling water (1 liter of water, 1 hour of stirring) and then again with acetone (1 liter, 1 hour of stirring).
The polymer is then dried under vacuum at about 100° C. till constant weight. It is obtained in an essentially quantitative yield.
The tables that follow list additional polymers prepared by the methods discussed above.
Example 3
This example illustrates the preparation of a poly(aryl ether) using the electrophilic polycondensation method. ##STR21## A three-liter glass lined reactor is charged with 0.50 moles of diphenyl ether (38), 0.50 moles of naphthalene-1,5-dicarbonyl chloride (37) and 1650 ml of 1,2-dichloroethane. The mixture is cooled to 0.5° C. and 1.55 moles of aluminum chloride are slowly added while maintaining the temperature between 0°-5° C. The resulting reaction mixture is held at 5°-10° C. for about 7 hours. At the end of this period the ice bath is removed, and the reaction mixture is allowed to warm to ambient temperature (25° C.) where it is held for an additional 16 hours. The reaction mixture is poured into 6 liters of ice water containing 200 ml of concentrated hydrochloric acid. The resulting multiphase system is heated to about 85° C. to distill the 1,2-dichloroethane. The polymer (39) is isolated by filtration, washed with water (2×1500 ml) and methanol (2×1500 ml), and dried in a vacuum oven at 100° C. It is obtained in an essentially quantitative yield.
                                  TABLE I                                 
__________________________________________________________________________
Preparation of Poly(aryl ethers)                                          
Via the Ullman Reaction                                                   
Example No.                               Starting Materials              
__________________________________________________________________________
        ##STR22##                                                         
                                           ##STR23##                      
        ##STR24##                                                         
                                           ##STR25##                      
        ##STR26##                                                         
                                           ##STR27##                      
        ##STR28##                                                         
                                           ##STR29##                      
        ##STR30##                                                         
                                           ##STR31##                      
        ##STR32##                                                         
                                           ##STR33##                      
10.                                                                       
        ##STR34##                                                         
                                           ##STR35##                      
        ##STR36##                                                         
                                           ##STR37##                      
        ##STR38##                                                         
                                           ##STR39##                      
        ##STR40##                                                         
                                           ##STR41##                      
        ##STR42##                                                         
                                           ##STR43##                      
        ##STR44##                                                         
                                           ##STR45##                      
        ##STR46##                                                         
                                           ##STR47##                      
        ##STR48##                                                         
                                           ##STR49##                      
        ##STR50##                                                         
                                           ##STR51##                      
        ##STR52##                                                         
                                           ##STR53##                      
20.                                                                       
        ##STR54##                                                         
                                           ##STR55##                      
        ##STR56##                                                         
                                           ##STR57##                      
        ##STR58##                                                         
                                           ##STR59##                      
        ##STR60##                                                         
                                           ##STR61##                      
        ##STR62##                                                         
                                           ##STR63##                      
        ##STR64##                                                         
                                           ##STR65##                      
        ##STR66##                                                         
                                           ##STR67##                      
__________________________________________________________________________
                                  TABLE II                                
__________________________________________________________________________
Preparation of Poly(aryl ethers) Via the Nickel Coupling Reaction         
Example No.                                                               
        Reagents                                                          
__________________________________________________________________________
         ##STR68##                                                        
         ##STR69##                                                        
         ##STR70##                                                        
__________________________________________________________________________
                                  TABLE III                               
__________________________________________________________________________
Preparation of Poly(aryl ethers) Via the Nucleophilic Polymerization      
Example No.                                                               
        Reagents                                                          
__________________________________________________________________________
30.                                                                       
         ##STR71##                                                        
         ##STR72##                                                        
         ##STR73##                                                        
         ##STR74##                                                        
         ##STR75##                                                        
         ##STR76##                                                        
         ##STR77##                                                        
         ##STR78##                                                        
         ##STR79##                                                        
         ##STR80##                                                        
40.                                                                       
         ##STR81##                                                        
         ##STR82##                                                        
         ##STR83##                                                        
         ##STR84##                                                        
         ##STR85##                                                        
         ##STR86##                                                        
         ##STR87##                                                        
         ##STR88##                                                        
         ##STR89##                                                        
         ##STR90##                                                        
50.                                                                       
         ##STR91##                                                        
__________________________________________________________________________
                                  TABLE IV                                
__________________________________________________________________________
Preparation of Poly(aryl ethers)                                          
Via the Electrophilic Route                                               
Example No.                         Reagents                              
__________________________________________________________________________
        ##STR92##                                                         
                                     ##STR93##                            
        ##STR94##                                                         
                                     ##STR95##                            
        ##STR96##                                                         
                                     ##STR97##                            
        ##STR98##                                                         
                                     ##STR99##                            
        ##STR100##                                                        
                                     ##STR101##                           
        ##STR102##                                                        
                                     ##STR103##                           
__________________________________________________________________________

Claims (2)

What is claimed is:
1. Poly(aryl ethers) having repeating units of the formula
--E--O--E'--O--
wherein E is one or more: divalent aromatic radical selected from the group consisting of ##STR104## and E' is one or more divalent radical selected from the group consisting of: E, ##STR105## where A is the group ##STR106## p is an integer and is independently 1 or 2; m is independently 0 or 1 with the proviso that when m is 1 the linkage of the group A to the body of the E radical is via the carbonyl function of the A group, and n is an integer of 1 to 5; T and T1 can be the same or different and are independently hydrogen, C1 to C4 alkyl, C1 to C4 alkoxy, phenyl, α-styryl, α-methylstyryl or halogen; Q is independently a chemical bond, O, S, S--S, CH2 or CO, with the proviso that when E is a naphthylene containing group and both m's are zero and n is one, Q cannot be CO.
2. Poly(aryl ethers) having repeating units of the formula ##STR107## wherein T and T1 are independently hydrogen, C1 to C4 alkyl, C1 to C4 alkoxy, phenyl, α-styryl, α-methylstyryl or halogen and Q' is independently O or CO with the proviso that at least one Q' is an oxygen bridge.
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Cited By (62)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4990589A (en) * 1987-11-04 1991-02-05 Raychem Limited Poly(arylene ether ketones)
EP0428743A1 (en) * 1989-05-23 1991-05-29 Teijin Limited Poly(arylene ether ketone), method of its production, and its use
EP0447358A2 (en) * 1990-03-12 1991-09-18 Ciba-Geigy Ag Soluble polyarylene ether sulfones
US5081216A (en) * 1989-02-28 1992-01-14 Basf Aktiengesellschaft Preparation of polyaryl ether ketones by electrophilic polycondensation
US5102971A (en) * 1988-06-25 1992-04-07 Bayer Aktiengesellschaft Soluble polyaromatic compounds
US5122588A (en) * 1989-03-04 1992-06-16 Basf Aktiengesellschaft Preparation of polyaryl ether ketones by electrophilic polycondensation
US5145938A (en) * 1987-11-17 1992-09-08 Raychem Limited Preparation of poly(arylene ether ketones)
US5153300A (en) * 1991-07-17 1992-10-06 General Electric Company Dihydroxy-meta-terphenyl polyesters and method of making
US5191056A (en) * 1990-08-17 1993-03-02 Teijin Limited Arylene sulfide ketone copolymer and preparation process thereof
US5204442A (en) * 1991-02-06 1993-04-20 General Electric Company Polyether polymers derived from 4,4"-dihydroxy-m-terphenyls
US5612451A (en) * 1994-07-11 1997-03-18 Basf Aktiengesellschaft Amphoteric metal oxides as cocatalyst in the electrophilic synthesis of polyaryl ether ketones
US6051661A (en) * 1997-01-24 2000-04-18 Basf Aktiengesellschaft Thermoplastic molding compositions
US20030069371A1 (en) * 1999-12-16 2003-04-10 Martin Weber Polyarylethersulphone and polyamide-based thermoplastic mouldable masses with improved processing characteristics
WO2009000741A1 (en) 2007-06-22 2008-12-31 Basf Se Molding materials comprising polyaryl ethers with improved surface quality
US20090275725A1 (en) * 2006-06-22 2009-11-05 Basf Se Polysulphones and polyether sulphones with reduced yellow index and processes for their preparation
US20100286303A1 (en) * 2007-11-13 2010-11-11 Basf Se Method for producing polyaryl ethers
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US20110028626A1 (en) * 2009-07-31 2011-02-03 Chemtura Corporation Flame retardant halogenated aryl ether oligomer compositions and their production
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US20110184107A1 (en) * 2010-01-25 2011-07-28 Chemtura Corporation Flame retardant halogenated phenyl ethers
US8362127B2 (en) 2010-01-25 2013-01-29 Chemtura Corporation Flame retardant halogenated phenyl ethers
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US11602438B2 (en) 2008-04-05 2023-03-14 DePuy Synthes Products, Inc. Expandable intervertebral implant
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US11654033B2 (en) 2010-06-29 2023-05-23 DePuy Synthes Products, Inc. Distractible intervertebral implant
US11737881B2 (en) 2008-01-17 2023-08-29 DePuy Synthes Products, Inc. Expandable intervertebral implant and associated method of manufacturing the same
US11752009B2 (en) 2021-04-06 2023-09-12 Medos International Sarl Expandable intervertebral fusion cage
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WO2024008502A1 (en) 2022-07-06 2024-01-11 Basf Se Process for the production of polyarylene(ether)sulfones with improved performance
US11911287B2 (en) 2010-06-24 2024-02-27 DePuy Synthes Products, Inc. Lateral spondylolisthesis reduction cage
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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4639504A (en) * 1982-06-08 1987-01-27 Dart Industries Inc. Production of thermally stabilized aromatic polyesters

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4639504A (en) * 1982-06-08 1987-01-27 Dart Industries Inc. Production of thermally stabilized aromatic polyesters

Cited By (108)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4990589A (en) * 1987-11-04 1991-02-05 Raychem Limited Poly(arylene ether ketones)
US5145938A (en) * 1987-11-17 1992-09-08 Raychem Limited Preparation of poly(arylene ether ketones)
US5102971A (en) * 1988-06-25 1992-04-07 Bayer Aktiengesellschaft Soluble polyaromatic compounds
US5081216A (en) * 1989-02-28 1992-01-14 Basf Aktiengesellschaft Preparation of polyaryl ether ketones by electrophilic polycondensation
US5122588A (en) * 1989-03-04 1992-06-16 Basf Aktiengesellschaft Preparation of polyaryl ether ketones by electrophilic polycondensation
EP0428743A1 (en) * 1989-05-23 1991-05-29 Teijin Limited Poly(arylene ether ketone), method of its production, and its use
US5290906A (en) * 1989-05-23 1994-03-01 Teijin Limited Poly(arylene ether ketone), process for producing same and its use
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US5191056A (en) * 1990-08-17 1993-03-02 Teijin Limited Arylene sulfide ketone copolymer and preparation process thereof
US5204442A (en) * 1991-02-06 1993-04-20 General Electric Company Polyether polymers derived from 4,4"-dihydroxy-m-terphenyls
US5153300A (en) * 1991-07-17 1992-10-06 General Electric Company Dihydroxy-meta-terphenyl polyesters and method of making
US5612451A (en) * 1994-07-11 1997-03-18 Basf Aktiengesellschaft Amphoteric metal oxides as cocatalyst in the electrophilic synthesis of polyaryl ether ketones
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US20030069371A1 (en) * 1999-12-16 2003-04-10 Martin Weber Polyarylethersulphone and polyamide-based thermoplastic mouldable masses with improved processing characteristics
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US8389673B2 (en) 2009-07-31 2013-03-05 Chemtura Corporation Aryl ether oligomers and process for making aryl ether oligomers
WO2011014317A1 (en) 2009-07-31 2011-02-03 Chemtura Corporation Aryl ether oligomers and process for making aryl ether oligomers
US20110028626A1 (en) * 2009-07-31 2011-02-03 Chemtura Corporation Flame retardant halogenated aryl ether oligomer compositions and their production
US20110024703A1 (en) * 2009-07-31 2011-02-03 Chemtura Corporation Aryl ether oligomers and process for making aryl ether oligomers
US11607321B2 (en) 2009-12-10 2023-03-21 DePuy Synthes Products, Inc. Bellows-like expandable interbody fusion cage
DE102010062886A1 (en) 2009-12-16 2011-06-22 Basf Se, 67063 Use of polyarylene ether sulfone for impact modification of thermoplastic polyamides containing a fibrous or particulate filler
US8362127B2 (en) 2010-01-25 2013-01-29 Chemtura Corporation Flame retardant halogenated phenyl ethers
US20110184107A1 (en) * 2010-01-25 2011-07-28 Chemtura Corporation Flame retardant halogenated phenyl ethers
US10966840B2 (en) 2010-06-24 2021-04-06 DePuy Synthes Products, Inc. Enhanced cage insertion assembly
US11872139B2 (en) 2010-06-24 2024-01-16 DePuy Synthes Products, Inc. Enhanced cage insertion assembly
US11911287B2 (en) 2010-06-24 2024-02-27 DePuy Synthes Products, Inc. Lateral spondylolisthesis reduction cage
US11654033B2 (en) 2010-06-29 2023-05-23 DePuy Synthes Products, Inc. Distractible intervertebral implant
US11452607B2 (en) 2010-10-11 2022-09-27 DePuy Synthes Products, Inc. Expandable interspinous process spacer implant
EP2581404A1 (en) 2011-10-11 2013-04-17 Basf Se Thermoplastic moulding material and moulded parts made of same with improved wear resistance
WO2013053723A1 (en) 2011-10-11 2013-04-18 Basf Se Thermoplastic moulding composition and moulded parts produced therefrom with improved wear resistance
US8729164B2 (en) 2011-10-11 2014-05-20 Basf Se Thermoplastic molding composition and moldings produced therefrom with improved wear resistance
EP2669316A1 (en) 2012-05-29 2013-12-04 Basf Se Method for producing high performance thermoplasts with improved inherent colour
WO2013178628A1 (en) 2012-05-29 2013-12-05 Basf Se Method for producing high-performance thermoplastics with an improved natural colour
US9127160B2 (en) 2012-05-29 2015-09-08 Basf Se Process for producing high-performance thermoplastics with improved intrinsic color
WO2014102308A2 (en) 2012-12-28 2014-07-03 Basf Se Method for purifying a recycle stream from a system for producing polyarylene ether sulfones
USRE49973E1 (en) 2013-02-28 2024-05-21 DePuy Synthes Products, Inc. Expandable intervertebral implant, system, kit and method
US11850164B2 (en) 2013-03-07 2023-12-26 DePuy Synthes Products, Inc. Intervertebral implant
US11497619B2 (en) 2013-03-07 2022-11-15 DePuy Synthes Products, Inc. Intervertebral implant
US10144807B2 (en) 2013-05-02 2018-12-04 Basf Se Block copolymers
WO2014177638A2 (en) 2013-05-02 2014-11-06 Basf Se Block copolymers
US10759908B2 (en) 2013-06-03 2020-09-01 Basf Se Polymers for membranes
US10058823B2 (en) 2013-06-03 2018-08-28 Basf Se Membranes
US10189943B2 (en) 2014-03-06 2019-01-29 Basf Se Copolymers suitable for making membranes
US10441925B2 (en) 2014-08-12 2019-10-15 Basf Se Process for making membranes
US10569232B2 (en) 2014-10-31 2020-02-25 Basf Se Copolymers for making membranes
WO2016066661A1 (en) 2014-10-31 2016-05-06 Basf Se Copolymers for making membranes
US11426290B2 (en) 2015-03-06 2022-08-30 DePuy Synthes Products, Inc. Expandable intervertebral implant, system, kit and method
WO2017045985A1 (en) 2015-09-17 2017-03-23 Basf Se Process for making membranes using lactam ide based solvents
US10906012B2 (en) 2015-09-17 2021-02-02 Basf Se Process for making membranes
US11596522B2 (en) 2016-06-28 2023-03-07 Eit Emerging Implant Technologies Gmbh Expandable and angularly adjustable intervertebral cages with articulating joint
US11596523B2 (en) 2016-06-28 2023-03-07 Eit Emerging Implant Technologies Gmbh Expandable and angularly adjustable articulating intervertebral cages
US11510788B2 (en) 2016-06-28 2022-11-29 Eit Emerging Implant Technologies Gmbh Expandable, angularly adjustable intervertebral cages
US10888433B2 (en) 2016-12-14 2021-01-12 DePuy Synthes Products, Inc. Intervertebral implant inserter and related methods
US11446155B2 (en) 2017-05-08 2022-09-20 Medos International Sarl Expandable cage
US11344424B2 (en) 2017-06-14 2022-05-31 Medos International Sarl Expandable intervertebral implant and related methods
US10940016B2 (en) 2017-07-05 2021-03-09 Medos International Sarl Expandable intervertebral fusion cage
US11446156B2 (en) 2018-10-25 2022-09-20 Medos International Sarl Expandable intervertebral implant, inserter instrument, and related methods
US11806245B2 (en) 2020-03-06 2023-11-07 Eit Emerging Implant Technologies Gmbh Expandable intervertebral implant
US11426286B2 (en) 2020-03-06 2022-08-30 Eit Emerging Implant Technologies Gmbh Expandable intervertebral implant
US11850160B2 (en) 2021-03-26 2023-12-26 Medos International Sarl Expandable lordotic intervertebral fusion cage
US12023258B2 (en) 2021-04-06 2024-07-02 Medos International Sarl Expandable intervertebral fusion cage
US11752009B2 (en) 2021-04-06 2023-09-12 Medos International Sarl Expandable intervertebral fusion cage
WO2023006830A1 (en) 2021-07-30 2023-02-02 Basf Se Polyarylether copolymers based on diols sugar alcohols
WO2023084062A1 (en) 2021-11-15 2023-05-19 Basf Se Polyarylether copolymers based on diol sugar alcohols
US12090064B2 (en) 2022-03-01 2024-09-17 Medos International Sarl Stabilization members for expandable intervertebral implants, and related systems and methods
WO2024008502A1 (en) 2022-07-06 2024-01-11 Basf Se Process for the production of polyarylene(ether)sulfones with improved performance

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